Apparatus for volumetrically controlling the flow of a gas and liquid mixture

Claim 2

Apparatus for volumetrically controlling the flow of a vapor and liquid mixture comprising: an inlet and at least two outlets, a first outlet being a liquid outlet and the second outlet being a vapor outlet; volumetric liquid control means for maintaining a predetermined constant volume of liquid flowing between the inlet and liquid outlet independent of changes in liquid pressure; separation means for separating liquid from vapor and located between the inlet and the liquid control means; liquid back pressure sensing means for sensing liquid back pressure downstream of the volumetric liquid control means; vapor dump control means for controlling the dumping of vapor through the vapor outlet and located between the separation means and the vapor outlet; vapor pressure sensing means for sensing pressure between the separation means and vapor control means; and the vapor dump control means adapted for operating in response to the liquid back pressure sensing means and vapor pressure sensing means to progressively increase vapor flow through the vapor outlet at higher liquid back pressures.

Claim 3

The apparatus of claim 1 wherein the liquid back pressure sensing means senses the liquid back pressure between a liquid shutoff means and the liquid outlet to open the vapor dump control means, the vapor pressure sensing means is adapted to oppose the pressure sensed by the liquid back pressure sensing means, and the vapor dump control means cooperates with the vapor pressure sensing means to control the vapor flow rate in relation to the system pressure.

Claim 4

The apparatus of claim 2 wherein the separation means includes: a circular horizontal receiver with an inlet disposed tangential to a receiver such that the liquid in the receiver continually changes direction inwardly; a spill ring formed by the upper edge of a substantially conical section depending from the receiver; a floor at the bottom of the conical section being downwardly helical in the direction of flow; and an outlet set on a tangent to the floor to receive liquid such that it retains its kinetic energy.

Claim 5

The apparatus of claim 3 wherein: the liquid control means is adjustable by a metering slot in a metering barrel so arranged to receive unmetered liquid into the bore of the barrel where it flows across the metering slot through a metering port; means to read the velocity across the metering port is provided; the liquid velocity is controlled by a throttle valve mounted off-center on a throttle diaphragm such that a pressure difference across the diaphragm causes the diaphragm to tilt and thereby open the throttle valve; the low pressure side of the throttle diaphragm has communication with a chamber between the throttle valve and a shutoff valve across an orifice and the throttle valve is thereby normally open; the control means further includes a spring loaded throttle control diaphragm operating a normally closed throttle control valve; the opening side of the throttle control diaphragm communicates with a point upstream of the metering barrel; the closing side of the throttle control diaphragm communicates with the downstream side of the metering barrel; and the throttle control valve opens into the low pressure side of the throttle diaphragm, such that the greater the velocity across the metering port, the greater the flow across the throttle control valve replenishing liquid on low pressure side of throttle diaphragm to close the throttle valve, and the throttle is thereby positioned valve to maintain a constant velocity across the metering barrel.

Claim 6

The apparatus of claim 4 wherein: a vapor dump chamber surrounds the separation means such that dumped vapor on its way to the vapor outlet can receive energy from the unmetered liquid.

Claim 7

The apparatus of claim 5 wherein: the chambers associated with the liquid outlet and the liquid control means have at least one connecting and common wall with a portion of the conical section of the receiver such that energy removal from the unmetered ammonia is provided at low demands regardless of vapor flow.